Injection Mold Having a Simplified Evaporative Cooling System or a Simplified Cooling System with Exotic Cooling Fluids

ABSTRACT

An injection mold assembly for a high output consumer product injection molding machine, the injection mold assembly having a simplified cooling system that is an evaporative cooling system or a cooling system including a hazardous, dangerous, or expensive cooling fluid. The simplified cooling system has a cooling fluid channel that is confined to a mold support plate.

CROSS REFERENCE TO RELATED APPLICATION

This application claims the benefit of U.S. Provisional Application No.61/641,349, filed May 2, 2012 which is hereby incorporated by reference.

TECHNICAL FIELD

The present invention relates to injection molds, more particularly, toinjection molds having a simplified evaporative cooling system.

BACKGROUND

Injection molding is a technology commonly used for high-volumemanufacturing of parts made of meltable material, most commonly of partsmade of thermoplastic polymers. During a repetitive injection moldingprocess, a plastic resin, most often in the form of small beads orpellets, is introduced to an injection molding machine that melts theresin beads under heat, pressure, and shear. The now molten resin isforcefully injected into a mold cavity having a particular cavity shape.The injected plastic is held under pressure in the mold cavity, cooled,and then removed as a solidified part having a shape that essentiallyduplicates the cavity shape of the mold. The mold itself may have asingle cavity or multiple cavities. Each cavity may be connected to aflow channel by a gate, which directs the flow of the molten resin intothe cavity. Thus, a typical injection molding procedure comprises fourbasic operations: (1) heating the plastic in the injection moldingmachine to allow it to flow under pressure; (2) injecting the meltedplastic into a mold cavity or cavities defined between two mold halvesthat have been closed; (3) allowing the plastic to cool and harden inthe cavity or cavities while under pressure; and (4) opening the moldhalves to allow the part to be ejected from the mold.

The molten plastic resin is injected into the mold cavity and theplastic resin is forcibly pushed through the cavity by the injectionmolding machine until the plastic resin reaches the location in thecavity furthest from the gate. The resulting length and wall thicknessof the part is a result of the shape of the mold cavity.

The molds used in injection molding machines must be capable ofwithstanding these high melt pressures. Moreover, the material formingthe mold must have a fatigue limit that can withstand the maximum cyclicstress for the total number of cycles a mold is expected to run over thecourse of its lifetime. As a result, mold manufacturers typically formthe mold from materials having high hardness, such as tool steels,having greater than 30 Rc, and more often greater than 50 Rc. These highhardness materials are durable and equipped to withstand the highclamping pressures required to keep mold components pressed against oneanother during the plastic injection process. Additionally, these highhardness materials are better able to resist wear from the repeatedcontact between molding surfaces and polymer flow.

High production injection molding machines (i.e., class 101 and class102 molding machines) that produce thinwalled consumer productsexclusively use molds having a majority of the mold made from the highhardness materials. High production injection molding machines typicallyproduce 500,000 parts or more. Industrial quality production molds mustbe designed to produce at least 500,000 parts, preferably more than1,000,000 parts, more preferably more than 5,000,000 parts, and evenmore preferably more than 10,000,000 parts. These high productioninjection molding machines have multi cavity molds and complex coolingsystems to increase production rates. The high hardness materialsdescribed above are more capable of withstanding the repeated highpressure clamping and injection operations than lower hardnessmaterials. However, high hardness materials, such as most tool steels,have relatively low thermal conductivities, generally less than 20BTU/HR FT ° F., which leads to long cooling times as heat is transferredfrom the molten plastic material through the high hardness material to acooling fluid.

In an effort to reduce cycle times, typical high production injectionmolding machines having molds made of high hardness materials includerelatively complex internal cooling systems that circulate cooling fluidwithin the mold. These cooling systems accelerate cooling of the moldedparts, thus allowing the machine to complete more cycles in a givenamount of time, which increases production rates and thus the totalamount of molded parts produced. However, these cooling systems addcomplexity and cost to the injection molds. In some class 101 molds morethan 1 or 2 million parts may be produced, these molds are sometimesreferred to as “ultra high productivity molds” Class 101 molds that runin 400 ton or larger presses are sometimes referred to as “400 class”molds within the industry.

High hardness materials are generally fairly difficult to machine. As aresult, known high throughput injection molds require extensivemachining time and expensive machining equipment to form, and expensiveand time consuming post-machining steps to relieve stresses and optimizematerial hardness. Milling and/or forming cooling channels within thesecomplex molds adds even more time and costs to the manufacture oftypical high throughput injection molds.

There is a tradeoff between machining complexity and cooling efficiencyin traditional, high hardness molds. Ideally, cooling channels should bemachined as close to the mold cavity surfaces as possible. Additionally,conformal cooling is desirable and most effective. However, machiningconformal cooling channels close to molding surfaces is difficult, timeconsuming, and expensive. Generally, machining cooling channels withinabout 5 mm of the mold surfaces is considered to be the practical limit.This practical limit reduces cooling efficiency due to material betweenthe cooling fluid and the hot plastic having low thermal conductivity.Conventional machining techniques, along with conventional moldmaterials (i.e., high hardness and low thermal conductivity) place alower limit on cycle time and cooling efficiency for a given mold.

Furthermore, locating cooling lines close to the mold surfaces requiresprecise machining of the cooling lines in the molds. Because the moldsare supported by mold support plates when placed in a clamping device ofthe injection molding machine, fluid seals must be located where thecooling lines transition from the mold support plate to the mold(because the fluid circulating systems (e.g., pumps) must be locatedoutside of the molds). These fluid seals may fail, causing cooling fluidto escape. As a result, parts may be incompletely cooled, which producesan inferior part, or the plastic in the mold may be contaminated withcooling fluid, which is also undesirable.

Still further, practical limitations on machining cooling channelsresults in unequal cooling within the mold. As a result, temperaturegradients are produced within the mold cavity. Often the temperature ofthe surface of a mold cavity can vary by ten degrees Celsius or more.This wide variation in temperature within the mold can lead toimperfections in the molded parts.

BRIEF DESCRIPTION OF THE DRAWINGS

The embodiments set forth in the drawings are illustrative and exemplaryin nature and not intended to limit the subject matter defined by theclaims. The following detailed description of the illustrativeembodiments can be understood when read in conjunction with thefollowing drawings, where like structure is indicated with likereference numerals and in which:

FIG. 1 illustrates a schematic view of an injection molding machineconstructed according to the disclosure;

FIG. 2 illustrates one embodiment of a thin-walled part formed in theinjection molding machine of FIG. 1;

FIG. 3 is a cavity pressure vs. time graph for a mold cavity in a moldof the injection molding machine of FIG. 1;

FIG. 4 is a cross-sectional view of one embodiment of a mold assembly ofthe injection molding machine of FIG. 1;

FIGS. 5A-5E illustrate different views of various mold assemblies havinga plurality of cooling lines machined in a mold support plate;

FIG. 6 illustrates a cross-sectional view of a mold assembly having aplurality of cooling lines machined in a mold support plate that extendinto a mold side;

FIG. 7 illustrates a close-up sectional view of a cooling line includinga baffle;

FIG. 8 illustrates a perspective cross-sectional view of a mold assemblyincluding a plurality of cooling lines machined along at least twodifferent axes;

FIG. 9 illustrates a perspective cross-sectional view of a mold assemblyhaving a plurality of terminal cooling lines and a plurality of throughbore cooling lines machined along at least two different machining axes;

FIG. 10 illustrates a perspective partially transparent view of a moldassembly having a plurality of cooling lines, at least one of thecooling lines being formed by two terminal cooling lines that join oneanother at terminal ends to form a non-terminal cooling line, eachterminal cooling line being machined along a different machining axis;

FIG. 11 illustrates a perspective view of a mold assembly having anactively cooled dynamic part;

FIG. 12 illustrates a perspective view of a mold assembly having atleast one cooling line that includes non-linear, non-coaxial, ornon-planar cooling channel;

FIG. 13 illustrates one embodiment of a cube mold that incorporates amold having a simplified cooling system;

FIG. 14 illustrates one embodiment of a vapor compression evaporativecooling system;

FIG. 15 illustrates another embodiment of an evaporative cooling system;

FIG. 16A illustrates an embodiment of an evaporative cooling systemcontained, at least partially, within a mold support plate;

FIG. 16B illustrates an alternate embodiment of an evaporative coolingsystem contained, at least partially, within a mold support plate; and

FIG. 17 illustrates one embodiment of an external evaporative coolingsystem.

DETAILED DESCRIPTION

Embodiments of the present invention generally relate to systems,machines, products, and methods of producing products by injectionmolding and more specifically to systems, products, and methods ofproducing products by low constant pressure injection molding.

The term “low pressure” as used herein with respect to melt pressure ofa thermoplastic material, means melt pressures in a vicinity of a nozzleof an injection molding machine of 6000 psi and lower.

The term “substantially constant pressure” as used herein with respectto a melt pressure of a thermoplastic material, means that deviationsfrom a baseline melt pressure do not produce meaningful changes inphysical properties of the thermoplastic material. For example,“substantially constant pressure’ includes, but is not limited to,pressure variations for which viscosity of the melted thermoplasticmaterial do not meaningfully change. The term “substantially constant”in this respect includes deviations of approximately 30% from a baselinemelt pressure. For example, the term “a substantially constant pressureof approximately 4600 psi” includes pressure fluctuations within therange of about 6000 psi (30% above 4600 psi) to about 3200 psi (30%below 4600 psi). A melt pressure is considered substantially constant aslong as the melt pressure fluctuates no more than 30% from the recitedpressure.

Referring to the figures in detail, FIG. 1 illustrates an exemplary lowconstant pressure injection molding apparatus 10 for producingthin-walled parts in high volumes (e.g., a class 101 or 102 injectionmold, or an “ultra high productivity mold”). The injection moldingapparatus 10 generally includes an injection system 12 and a clampingsystem 14. A thermoplastic material may be introduced to the injectionsystem 12 in the form of thermoplastic pellets 16. The thermoplasticpellets 16 may be placed into a hopper 18, which feeds the thermoplasticpellets 16 into a heated barrel 20 of the injection system 12. Thethermoplastic pellets 16, after being fed into the heated barrel 20, maybe driven to the end of the heated barrel 20 by a reciprocating screw22. The heating of the heated barrel 20 and the compression of thethermoplastic pellets 16 by the reciprocating screw 22 causes thethermoplastic pellets 16 to melt, forming a molten thermoplasticmaterial 24. The molten thermoplastic material is typically processed ata temperature of about 130° C. to about 410° C.

The reciprocating screw 22 forces the molten thermoplastic material 24,toward a nozzle 26 to form a shot of thermoplastic material, which willbe injected into a mold cavity 32 of a mold 28. The molten thermoplasticmaterial 24 may be injected through a gate 30, which directs the flow ofthe molten thermoplastic material 24 to the mold cavity 32. The moldcavity 32 is formed between first and second mold parts 25, 27 of themold 28 and the first and second mold parts 25, 27 are held togetherunder pressure by a press or clamping unit 34. The press or clampingunit 34 applies a clamping force in the range of approximately 1000 psito approximately 6000 psi during the molding process to hold the firstand second mold parts 25, 27 together while the molten thermoplasticmaterial 24 is injected into the mold cavity 32. To support theseclamping forces, the clamping system 14 may include a mold frame and amold base, the mold frame and the mold base being formed from a materialhaving a surface hardness of more than about 165 BHN and preferably lessthan 260 BHN, although materials having surface hardness BHN values ofgreater than 260 may be used as long as the material is easilymachineable, as discussed further below.

Once the shot of molten thermoplastic material 24 is injected into themold cavity 32, the reciprocating screw 22 stops traveling forward. Themolten thermoplastic material 24 takes the form of the mold cavity 32and the molten thermoplastic material 24 cools inside the mold 28 untilthe thermoplastic material 24 solidifies. Once the thermoplasticmaterial 24 has solidified, the press 34 releases the first and secondmold parts 25, 27, the first and second mold parts 25, 27 are separatedfrom one another, and the finished part may be ejected from the mold 28.The mold 28 may include a plurality of mold cavities 32 to increaseoverall production rates.

A controller 50 is communicatively connected with a sensor 52 and ascrew control 36. The controller 50 may include a microprocessor, amemory, and one or more communication links. The controller 50 may beconnected to the sensor 52 and the screw control 36 via wiredconnections 54, 56, respectively. In other embodiments, the controller50 may be connected to the sensor 52 and screw control 56 via a wirelessconnection, a mechanical connection, a hydraulic connection, a pneumaticconnection, or any other type of communication connection known to thosehaving ordinary skill in the art that will allow the controller 50 tocommunicate with both the sensor 52 and the screw control 36.

In the embodiment of FIG. 1, the sensor 52 is a pressure sensor thatmeasures (directly or indirectly) melt pressure of the moltenthermoplastic material 24 in the nozzle 26. The sensor 52 generates anelectrical signal that is transmitted to the controller 50. Thecontroller 50 then commands the screw control 36 to advance the screw 22at a rate that maintains a substantially constant melt pressure of themolten thermoplastic material 24 in the nozzle 26. While the sensor 52may directly measure the melt pressure, the sensor 52 may measure othercharacteristics of the molten thermoplastic material 24, such astemperature, viscosity, flow rate, etc, that are indicative of meltpressure. Likewise, the sensor 52 need not be located directly in thenozzle 26, but rather the sensor 52 may be located at any locationwithin the injection system 12 or mold 28 that is fluidly connected withthe nozzle 26. If the sensor 52 is not located within the nozzle 26,appropriate correction factors may be applied to the measuredcharacteristic to calculate the melt pressure in the nozzle 26. In yetother embodiments, the sensor 52 need not be fluidly connected with thenozzle. Rather, the sensor could measure clamping force generated by theclamping system 14 at a mold parting line between the first and secondmold parts 25, 27.

Although an active, closed loop controller 50 is illustrated in FIG. 1,other pressure regulating devices may be used instead of the closed loopcontroller 50. For example, a pressure regulating valve (not shown) or apressure relief valve (not shown) may replace the controller 50 toregulate the melt pressure of the molten thermoplastic material 24. Morespecifically, the pressure regulating valve and pressure relief valvecan prevent overpressurization of the mold 28. Another alternativemechanism for preventing overpressurization of the mold 28 is an alarmthat is activated when an overpressurization condition is detected.

Turning now to FIG. 2, an example molded part 100 is illustrated. Themolded part 100 is a thin-walled part. Molded parts are generallyconsidered to be thin-walled when a length of a flow channel L dividedby a thickness of the flow channel T is greater than 100 (i.e.,L/T>100). The low constant pressure injection molding systems and moldshaving simplified cooling that are described herein become increasinglyadvantageous for molding parts as L/T ratios increase, particularly forparts having L/T>200, or L/T>250 because the molten thermoplasticmaterial includes a continuous flow front that advances through the moldcavity, which fills the mold cavity with thermoplastic material moreconsistently than high variable pressure injection molding systems. Thelength of the flow channel L is measured from a gate 102 to a flowchannel end 104. Thin-walled parts are especially prevalent in theconsumer products industry and healthcare or medical supplies industry.

Thin-walled parts present certain obstacles in injection molding. Forexample, the thinness of the flow channel tends to cool the moltenthermoplastic material before the material reaches the flow channel end104. When this happens, the thermoplastic material freezes off and nolonger flows, which results in an incomplete part. To overcome thisproblem, traditional injection molding machines inject the moltenthermoplastic material into the mold at very high pressures, typicallygreater than 15,000 psi, so that the molten thermoplastic materialrapidly fills the mold cavity before having a chance to cool and freezeoff. This is one reason that manufacturers of the thermoplasticmaterials teach injecting at very high pressures. Another reasontraditional injection molding machines inject molten plastic into themold at high pressures is the increased shear, which increases flowcharacteristics, as discussed above. These very high injection pressuresrequire the use of very hard materials to form the mold 28 and the feedsystem.

Traditional injection molding machines use molds made of tool steels orother hard materials to make the mold. While these tool steels arerobust enough to withstand the very high injection pressures, toolsteels are relatively poor thermal conductors. As a result, very complexcooling systems are machined into the molds to enhance cooling timeswhen the mold cavity is filled, which reduces cycle times and increasesproductivity of the mold. However, these very complex cooling systemsadd great time and expense to the mold making process.

The inventors have discovered that shear-thinning thermoplastics (evenminimally shear-thinning thermoplastics) may be injected into the mold28 at low, substantially constant, pressure without any significantadverse affects. Examples of these materials include but are not limitedto polymers and copolymers comprised of, polyolefins (e.g.,polypropylene, polyethylene), thermoplastic elastomers, polyesters (e.g.polyethelyne terephthalate, polybutelene terephthalate), polystyrene,polycarbonate, poly(acrylonitrile-butadiene-styrene), poly(latic acid),polyhydroxyalkanoate, polyamides, polyacetals, ethylene-alpha olefinrubbers, and styrene-butadiene-stryene block copolymers. In fact, partsmolded at low, substantially constant, pressures exhibit some superiorproperties as compared to the same part molded at a conventional highpressure. This discovery directly contradicts conventional wisdom withinthe industry that teaches higher injection pressures are better. Withoutbeing bound by theory, it is believed that injecting the moltenthermoplastic material into the mold 28 at low, substantially constant,pressures creates a continuous flow front of thermoplastic material thatadvances through the mold from a gate to a farthest part of the moldcavity. By maintaining a low level of shear, the thermoplastic materialremains liquid and flowable at much lower temperatures and pressuresthan is otherwise believed to be possible in conventional high pressureinjection molding systems.

Turning now to FIG. 3, a typical pressure-time curve for a conventionalhigh pressure injection molding process is illustrated by the dashedline 200. By contrast, a pressure-time curve for the disclosed lowconstant pressure injection molding machine is illustrated by the solidline 210.

In the conventional case, melt pressure is rapidly increased to wellover 15,000 psi and then held at a relatively high pressure, more than15,000 psi, for a first period of time 220. The first period of time 220is the fill time in which molten plastic material flows into the moldcavity. Thereafter, the melt pressure is decreased and held at a lower,but still relatively high pressure, 10,000 psi or more, for a secondperiod of time 230. The second period of time 230 is a packing time inwhich the melt pressure is maintained to ensure that all gaps in themold cavity are back filled. The mold cavity in a conventional highpressure injection molding system is filled from the end of the flowchannel back to towards the gate. As a result, plastic in various stagesof solidification are packed upon one another, which may causeinconsistencies in the finished product, as discussed above. Moreover,the conventional packing of plastic in various stages of solidificationresults in some non-ideal material properties, for example, molded-instresses, sink, and non-optimal optical properties.

The constant low pressure injection molding system, on the other hand,injects the molten plastic material into the mold cavity at asubstantially constant low pressure for a single time period 240. Theinjection pressure is less than 6,000 psi. By using a substantiallyconstant low pressure, the molten thermoplastic material maintains acontinuous melt front that advances through the flow channel from thegate towards the end of the flow channel. Thus, the plastic materialremains relatively uniform at any point along the flow channel, whichresults in a more uniform and consistent finished product. By fillingthe mold with a relatively uniform plastic material, the finished moldedparts may form crystalline structures that have better mechanical and/orbetter optical properties than conventionally molded parts. Amorphouspolymers may also form structures having superior mechanical and/oroptical properties. Moreover, the skin layers of parts molded at lowconstant pressures exhibit different characteristics than skin layers ofconventionally molded parts. As a result, the skin layers of partsmolded under low constant pressure can have better optical propertiesthan skin layers of conventionally molded parts.

By maintaining a substantially constant and low (e.g., less than 6000psi) melt pressure within the nozzle, more machineable materials may beused to form the mold 28. For example, the mold 28 illustrated in FIG. 1may be formed of a material having a milling machining index of greaterthan 100%, a drilling machining index of greater than 100%, a wire EDMmachining index of greater than 100%, a graphite sinker EDM machiningindex of greater than 200%, or a copper sinker EDM machining index ofgreater than 150%. The machining indexes are based upon milling,drilling, wire EDM, and sinker EDM tests of various materials. The testmethods for determining the machining indices are explained in moredetail below. Examples of machining indexes for a sample of materials iscompiled below in Table 1.

TABLE 1 Machining Technology Milling Drilling Spindle Spindle Wire EDMSinker EDM-Graphite Sinker EDM-Copper Load Index % Load Index % timeIndex % time Index % time Index % Material 1117* 0.72 100%  0.32 100% 9:34 100% 0:14:48 100% 0:24:00 100% 6061 Al 0.50 144%  0.20 160%  4:46201% 0:05:58 243% 0:15:36 154% 7075 Al 0.55 131%  0.24 133%  4:48 199%0:05:20 278% 0:12:27 193% Alcoa QC-10 Al 0.56 129%  0.24 133%  4:47 200%0:05:11 286% 0:12:21 194% 4140 0.92 78% 0.37 86% 9:28 101% 0:09:36 154%0:19:20 124% 420 SS 1.36 53% 0.39 82% 8:30 113% 0:10:12 145% 0:23:20103% A2 0.97 74% 0.45 71% 8:52 108% 0:08:00 185% 0:20:12 119% S7 1.2060% 0.43 74% 9:03 106% 0:12:53 115% 0:20:58 114% P20 1.10 65% 0.38 84%9:26 101% 0:11:47 126% 0:20:30 117% PX5 1.12 64% 0.37 86% 9:22 102%0:12:37 117% 0:23:18 103% Moldmax HH 0.80 90% 0.36 89% 6:00 159% 6:59:35 4% 1 0:43:38  55% 3 Ampcoloy 944 0.62 116%  0.32 100%  6:53 139%3:13:41  8% 2 0:30:21  79% 4 *1117 is the benchmark material for thistest. Published data references 1212 carbon steel as the benchmarkmaterial. 1212 was not readily available. Of the published data, 1117was the closest in composition and machining index percentage (91%). 1Significant graphite electrode wear: ^(~)20% 2 graphite electrode wear:^(~)15% 3 Cu electrode wear: ^(~)15% 4 Cu electrode wear: ^(~)3%

Using easily machineable materials to form the mold 28 results ingreatly decreased manufacturing time and thus, a decrease inmanufacturing costs. Moreover, these machineable materials generallyhave better thermal conductivity than tool steels, which increasescooling efficiency and decreases the need for complex cooling systems.

When forming the mold 28 of these easily machineable materials, it isalso advantageous to select easily machineable materials having goodthermal conductivity properties. Materials having thermal conductivitiesof more than 30 BTU/HR FT ° F. are particularly advantageous. Forexample easily machineable materials having good thermal conductivitiesinclude, but are not limited to, Alcoa QC-10, Alcan Duramold 500, andHokotol (available from Alerts). Materials with good thermalconductivity more efficiently transmit heat from the thermoplasticmaterial out of the mold. As a result, more simple cooling systems maybe used.

One example of a multi-cavity mold assembly 28 is illustrated in FIG. 4.Multi-cavity molds generally include a feed manifold 60 that directsmolten thermoplastic material from the nozzle 26 to the individual moldcavities 32. The feed manifold 60 includes a sprue 62, which directs themolten thermoplastic material into one or more runners or feed channels64. Each runner 64 may feed multiple mold cavities 32. High productivitymolds may include four or more mold cavities 32, sometimes as many asthree hundred and eighty four mold cavities 32, and often also mayinclude heated runners 64. Some embodiments of constant low pressureinjecting molding machines may include non-naturally balanced feedsystems, such as artificially balanced feed systems, or non-balancedfeed systems.

Drilling and Milling Machineability Index Test Methods

The drilling and milling machineability indices listed above in Table 1were determined by testing the representative materials in carefullycontrolled test methods, which are described below.

The machineability index for each material was determined by measuringthe spindle load needed to drill or mill a piece of the material withall other machine conditions (e.g., machine table feed rate, spindlerpm, etc.) being held constant between the various materials. Spindleload is reported as a ratio of the measured spindle load to the maximumspindle torque load of 75 ft-lb at 1400 rpm for the drilling or millingdevice. The index percentage was calculated as a ratio between thespindle load for 1117 steel to the spindle load for the test material.

The test milling or drilling machine was a Haas VF-3 Machining Center.

TABLE 2 Drilling Conditions Spot Drill 118 degree 0.5″ diameter, drilledto 0.0693″ depth Drill Bit 15/32″ diameter high speed steel uncoatedjobber length bit Spindle Speed 1200 rpm Depth of Drill 0.5″ Drill Rate3 in/min Other No chip break routine used

TABLE 3 Milling Conditions Mill 0.5″ diameter 4 flute carbide flatbottom end mill, uncoated (SGS part # 36432 www.sgstool.com) SpindleSpeed 1200 rpm Depth of Cut 0.5″ Stock Feed Rate 20 in/min

For all tests “flood blast” cooling was used. The coolant was Koolrite2290.

EDM Machineability Index Test Methods

The graphite and copper sinker EDM machineability indices listed abovein Table 1 were determined by testing the representative materials in acarefully controlled test method, which is described below.

The EDM machineability index for the various materials were determinedby measuring the time to burn an area (specifics below) into the varioustest metals. The machineability index percentage was calculated as theratio of the time to burn into 1117 steel to time required to burn thesame area into the other test materials.

TABLE 4 Wire EDM Equipment Fanuc OB Wire 0.25 mm diameter hard brass Cut1″ thick × 1″ length (1 sq. ″) Parameters Used Fanuc on board artificialintelligence, override at 100%

TABLE 5 Sinker EDM - Graphite Equipment Ingersoll Gantry 800 withMitsubishi EX Controller Wire System 3R pre-mounted 25 mm diameter PocoEDM 3 graphite Cut 0.1″ Z axis plunge Parameters Used Mitsubishi CNCcontrols with FAP EX Series Technology

TABLE 6 Sinker EDM - Copper Equipment Ingersoll Gantry 800 withMitsubishi EX Controller Wire System 3R pre-mounted 25 mm diameterTellurium Copper Cut 0.1″ Z axis plunge Parameters Used Mitsubishi CNCcontrols with FAP EX Series Technology

The disclosed low constant pressure injection molding machinesadvantageously employ molds constructed from easily machineablematerials. As a result, the disclosed low constant pressure injectionmolds (and thus the disclosed low constant pressure injection moldingmachines) are less expensive and faster to produce. Additionally, thedisclosed low constant pressure injection molding machines are capableof employing more flexible support structures and more adaptabledelivery structures, such as wider platen widths, increased tie barspacing, elimination of tie bars, lighter weight construction tofacilitate faster movements, and non-naturally balanced feed systems.Thus, the disclosed low constant pressure injection molding machines maybe modified to fit delivery needs and are more easily customizable forparticular molded parts.

Moreover, the disclosed low constant pressure injection molds (e.g.,mold assemblies that include one or more mold sides and one or more moldsupport plates) may include simplified cooling systems relative tocooling systems found in conventional high pressure injection molds. Thesimplified cooling systems are more economical than conventional coolingsystems because the simplified cooling systems are more quickly andeasily produced. Additionally, the simplified cooling systems use lesscoolant, which further reduces cooling costs during molding operations.In some cases, the simplified cooling systems may be located solely inthe mold support plates, which allows the mold sides to be changedwithout the need for changing the cooling system. In summary, thesimplified cooling systems of the disclosed low constant pressureinjection molding molds are more economical and more effective thanconventional complex cooling systems found in conventional high pressureinjection molds.

Generally speaking, a mold support plate physically supports andreinforces a mold side. Two or more mold sides (or mold cores) define amold cavity. A mold support plate may support a mold side by continuouscontact along a length and width of a mold side. Alternatively, a moldsupport plate may support a mold side by intermittent or partialphysical contact with the mold side. Such intermittent or partialphysical contact may be used for a variety of reasons such as (i) tofocus the load bearing contact on certain locations (e.g., reinforcedlocations) of the mold side, (ii) to direct the location of portions ofthe thermal exchange or heat flow between specific parts of the moldside and the mold support plate, or (iii) to accommodate the specialneeds for a given apparatus. The mold support plate may remain incontact with the mold side throughout the molding process, or the moldsupport plate may completely separate from the mold side for certainperiods of time during the molding process. Moreover, the mold supportplate may be formed of two or more separate pieces that are fixed to oneanother. The mold support plate may be made of a material with a highthermal conductivity (e.g., 30 BTU/hr Ft ° F.). In some embodiments, themold support plate may be made of a material having a higher thermalconductivity than the material of the mold side, or vice versa. In yetother embodiments, the mold support plate may have a thermalconductivity that is identical to the thermal conductivity of the moldside. In one example, the mold support plate may be made of CuBe, orleast a portion of the mold support plate may be made of CuBe, whichcontacts the mold side that may be made of aluminum. While the moldsupport plates illustrated in the drawings are generally formed from asingle piece of material, in other embodiments, the mold support platesmay be formed from multiple pieces of similar or different material thatare fixed to one another.

Cooling systems of all sorts may be categorized in a system of coolingcomplexity levels, with cooling complexity level zero representing themost simple cooling system and higher cooling complexity levelsrepresenting progressively more complex cooling systems. This system ofcooling system categorization is discussed below in more detail.However, conventional high productivity consumer product injectionmolding machines (e.g., class 101 and 102 molding machines) employcomplex cooling systems to reduce cycle time and improve productivity.Generally speaking, high productivity consumer product injection moldingmachines include complex cooling systems (i.e., cooling systems having alevel four cooling system complexity level or higher). Level zero tolevel three cooling complexity level systems generally do not producecooling capacity that is sufficient for conventional high productivityinjection molds, which include molds made of high hardness, low thermalconductivity materials.

Advantageously, the disclosed low constant pressure injection moldsinclude cooling systems having cooling complexity levels of three orless, preferably cooling complexity level three, two, or one, whichlowers production costs and increases efficiency over conventional highpressure injection molding machines.

As used herein, a cooling complexity level zero mold assembly is definedas a mold assembly that includes no active cooling system. In otherwords, a cooling complexity level zero mold assembly is only passivelycooled through the conduction of heat through the mold sides and throughthe mold support plates, and eventually to the atmosphere surroundingthe mold assembly. Cooling complexity level zero mold assembliestypically have relatively long cycle times (as it takes a significantamount of time for the plastic within the mold to freeze because of theslow cooling rate). As a result, high productivity consumer product moldassemblies (e.g., mold assemblies used in class 101-102 moldingmachines) do not use cooling complexity level zero mold assemblies.

Turning now to FIGS. 5A-5E, different embodiments of a coolingcomplexity level one mold assembly 328 (and/or different embodiments ofa mold support plate in the mold assembly) are illustrated. The moldassembly 328 may include a mold 370 having a first side 372 and a secondside 374. The first side 372 and the second side 374 form a mold cavity376 therebetween. The first side 372 may be supported by a first moldsupport plate 378 and the second side 374 may be supported by a secondmold support plate 380. The first and second mold support plates 378,380 may be attached to a press (not shown), which actuates to move thefirst and second sides 372, 374 during the molding process. One or morecooling lines 382 may be formed in one or more of the mold supportplates 378, 380. Because the first and second sides 372, 374 are madefrom a highly thermally conductive material, heat flows through thefirst and second sides 372, 374 to the mold support plates 378, 380 at arate that is sufficient to cool plastic in the mold cavity 376 in anacceptable amount of time.

The mold support plates 378, 380 may include posts or other projections381 that extend outward, away from the mold support plate 378, 380,towards the mold 370. The cooling lines 382 may extend into theprojections 381. The mold 370 may include a complementary feature sothat the mold may fit around (FIG. 5B), within (FIG. 5C), or upon (FIGS.5D and 5E) the projections 381. In this way, the cooling lines 382 maybe located closer to the mold cavity without extending the cooling lines382 into the mold 370 or into the first and second mold sides 372, 374.As a result, the mold support plates 378, 380 may receive molds having avariety of different mold cavity shapes. The molds may thus be formedwithout cooling lines integrated into the first and/or second sides 372,374, which reduces manufacturing costs of the molds 370.

Conventional high output consumer product injection mold assemblies donot use cooling complexity level one mold assemblies because such moldassemblies do not adequately cool plastic with in a mold cavity formedby two high hardness, low thermal conductivity materials. Coolingcomplexity level one mold assemblies are defined as containing allactive cooling lines 382 within the mold support plates 378, 380, evenif more than one machining axis is needed to form the cooling lines 382.In the example of FIGS. 5A-5E, the mold may be a stack mold, a cubemold, a shuttle mold, a helicopter mold, a mold having rotating platens,or other multi-cavity molds to increase productivity if desired.

Turning now to FIG. 6, a cooling complexity level two mold assembly 328is illustrated. The cooling complexity level two mold assembly 328 isidentical to the cooling complexity level one mold assembly 328 of FIGS.5A-5E, with the exception that the cooling lines 382 in the embodimentof FIG. 6 extend through at least one mold support plate 378, 380 andinto at least one mold side 372, 374 (i.e., as opposed to the coolinglines 382 only extending through the mold support plates 378, 380). Thecooling lines 382 have terminal ends 384. However, each cooling line 382is machined along an axis that is parallel to a single machining axis.The cooling lines 382 may include a baffle 386, as shown in more detailin FIG. 7, to facilitate cooling fluid flow through the cooling line382. Cooling complexity level two mold assemblies have not been used inhigh output consumer product injection molding machines (i.e., class101-102 injection molding machines) because cooling complexity level twomold assemblies do not have enough flexibility to machine cooling linesclose to the mold surfaces of the mold cavity and therefore, coolingcomplexity level two mold assemblies do not provide adequate cooling forconventional high output mold assemblies having high hardness, lowthermal conductivity molds.

Turning now to FIG. 8 an embodiment of a cooling complexity level threemold assembly 328 is illustrated. A cooling complexity level three moldassembly 328 is defined by cooling channels 382 having at least twodifferent machining axes. At least one cooling line 382 may include twodifferent machining axes and a terminal end. More particularly, thecooling line 382 may have a bend or turn. For example, the cooling line382 may include a first machining axis that is substantially parallel tothe opening-closing stroke S of the mold assembly 328 and a secondmachining axis that is angled with respect to the first machining axis.Like cooling complexity level two mold assemblies, cooling complexitylevel three mold assemblies have not been used in high output consumerproduct injection molding machines (e.g., class 101-102 injectionmolding machines) because level three cooling complexity does not haveenough flexibility to machine cooling lines close to the mold surfacesof the mold cavity and therefore, cooling complexity level three moldassemblies do not provide adequate cooling for conventional high outputmold assemblies having high hardness, low thermal conductivity molds.

Turning now to FIG. 9, a cooling complexity level four mold assembly 328is illustrated. The cooling complexity level four mold assembly 328includes a plurality of cooling lines 382, a first cooling line 382 ahaving a terminal end 384 and a second cooling line 382 b being athrough-bore without a terminal end. The first cooling line 382 aextends from the mold support plate 378 into the first mold side 372 andthe second cooling line 382 b extends through the first mold side 372. Amachining axis for the first cooling line 382 a is different from amachining axis for the second cooling line 382 b. In other words, thecooling lines 382 have at least two different machining axes forformation. Cooling complexity level four mold assemblies have been usedin some high output consumer product injection molding machines (e.g.,class 101-102 injection molding machines) having mold assemblies withvery simple mold cavity geometries.

Turning now to FIG. 10, a cooling complexity level five mold assembly328 is illustrated. The cooling complexity level five mold assembly 328includes a first cooling line 382 that is a through-bore having twodifferent machining axes. As illustrated in FIG. 10, the first coolingline 382 includes a first section 390 and a second section 392 that areangled with respect to one another and meet at a junction or turn 394.Machining the first cooling line 382 with two different axes that mustmeet at an internal location in the mold part requires great precisionand thus more costly equipment, along with a greater manufacturing time.However, cooling complexity level five mold assemblies 328 have beenused in high output consumer product injection molding machines (e.g.,class 101-102 injection molding machines) because cooling complexitylevel five mold assemblies allow for greater customization in coolingline placement. Thus, cooling lines can be placed closer to the moldcavity than in cooling complexity mold assemblies of lesser complexity.As a result, the more complex cooling complexity mold assembly can atleast partially offset the drawback of lower thermal conductivity foundin conventional injection molds made of high hardness, low thermalconductivity materials.

Turning now to FIG. 11, a cooling complexity level six mold assembly 328is illustrated. The cooling complexity level six mold assembly 328 is acooling complexity level one to five mold assembly that also includes atleast one actively cooled dynamic molding part 398. Forming coolingchannels in a dynamic molding part 398 requires great precision.Moreover, actively cooled dynamic molding parts 398 require complicatedflow mechanisms that move with the dynamic molding part 398 duringoperation of the mold assembly 328. Cooling complexity level six moldassemblies have been used in high output consumer product injectionmolding machines (e.g., class 101-102 injection molding machines).

Turning now to FIG. 12, a cooling complexity level seven mold assembly328 is illustrated. The cooling complexity level seven mold assembly 328is a cooling complexity level two through six mold assembly thatincludes at least one conformal cooling cavity 399. The conformalcooling cavity 399 at least partially complements the contours of themold cavity to provide maximum active cooling. The conformal coolingcavity 399 is non-linear, non-coaxial, and/or non-planar. Conformalcooling cavities 399 require complex machinery to form. Additionally,conformal cooling cavities 399 take significant amounts of time to form.As a result, cooling complexity level seven mold assemblies are veryexpensive and are generally reserved for high output consumer productinjection molding machines that have very intricate part geometries.

The simplified cooling systems described herein may be incorporated intovirtually any type of conventional injection mold, such as an injectionmolding machine having a cube mold assembly 428, as illustrated in FIG.13.

Returning now to FIGS. 5A-5E, in some embodiments, a level one coolingcomplexity level injection mold assembly may include an evaporativecooling system. Evaporative cooling systems are more efficient inremoving heat than liquid based cooling systems. In some examples,evaporative cooling systems may be 100 times more efficient, or even 500times more efficient, at removing heat than liquid based coolingsystems. Because the injection mold assemblies described herein are madeof materials having high thermal conductivity, these mold assemblies mayinclude more simplified cooling systems (by moving cooling lines fartheraway from the mold cavity) while increasing heat removal by includingevaporative cooling systems. Moving cooling lines away from the moldcavity produces more uniform temperature distributions throughout themold sides. Advantageously, level one cooling complexity mold assemblieshaving evaporative cooling systems do not need complex dynamic sealsbetween the mold support plates and the mold sides because the coolingfluid lines do not extend into the mold sides. As a result, theevaporative cooling systems in level one cooling complexity level moldassemblies are more robust and less prone to failure than evaporativecooling systems in prior art mold assemblies that required the coolingfluid to extend into the mold sides.

Generally speaking, evaporative cooling systems exploit a phase changein a cooling fluid to extract more heat from the mold assembly than aconventional all liquid cooling system could extract. By using localizedpressure differentials, the circulating fluid alternates between aliquid and a gas phase. Transition from a liquid to a gas phase ishighly endothermic. When the liquid cooling fluid passes through aregion of elevated temperature (such as the mold support plate, or anevaporator), the cooling fluid absorbs heat from the mold support plateand changes phase to a gas. The gas then passes to a region of lowertemperature, such as a condenser, where heat is transferred from the gasto the environment. This heat transfer causes the gas to condense backinto a liquid that may be pumped back into the mold support plate toabsorb more heat and the cycle is repeated. Evaporative cooling systemsmay be ten times more effective, 100 times, or even 500 times moreeffective at removing heat than conventional all liquid cooling systems.

More specifically, a refrigeration-type vapor compression cooling system500 is illustrated in FIG. 14. The vapor compression cooling system 500includes a compressor 510 that increases pressure of a cooling fluidwithin cooling lines 512 a,b of a cooling circuit 514, which causes thetemperature of the cooling fluid to rise in cooling line 512 a accordingto the combined gas law (i.e., p₁V₁/T₁=p₂V₂/T₂). After being compressed,the elevated temperature cooling fluid enters a heat exchanger orcondenser 516. The elevated temperature cooling fluid exchanges heatwith the atmosphere (or other medium), and the cooling fluid cools belowits evaporation temperature, thus condensing into liquid form. Theliquid cooling fluid then moves through cooling line 512 b to anexpansion valve 520, where the volume of the cooling liquid isincreased, causing the pressure of the cooling liquid to decrease, whichcauses the cooling fluid to at least partially evaporate, againaccording to the combined gas law. Some of the cooling fluid mayvaporize so that a combination of liquid and gas cooling fluid movesthrough cooling line 512 c to an evaporator 522. In one embodiment, amold support plate may comprise the evaporator 522. The mold supportplate may include one or more cooling channels for moving cooling fluidthrough the mold support plate to remove heat from the mold supportplate. The evaporator surfaces are relatively warm, compared to thecooling fluid in the evaporator 522. Thus, heat is transferred from theevaporator (e.g., the mold support plate) to the cooling fluid, whichresults in vaporization of a majority of the remaining cooling fluid.

After exchanging heat and vaporizing in the evaporator 522, the coolingfluid moves through cooling line 512 d to the compressor 510 and theprocess is repeated. The evaporator 522, the compressor 510, thecondenser 516, and the expansion valve 520 are all fluidly connected toone another by the cooling lines 512 a-d. In some embodiments, theentire cooling circuit 514 may be located within or on the evaporator522 or mold support plate. In other embodiments, the mold support platemay comprise the evaporator 522 (having one or more cooling channelslocated within the mold support plate), while one or more of thecompressor 510, the condenser 516, and the expansion valve 520 may bephysically separated from the mold support plate, while being fluidlyconnected to the mold support plate via the cooling lines 512 a-d.

FIG. 15 illustrates one embodiment of an evaporative cooling system 600that may be used in an injection molding machine. The evaporativecooling system 600 includes the same elements as the evaporative coolingsystem of FIG. 14, with respective elements having reference numeralsincreased by 100. The evaporative cooling system 600 includes acompressor 610, a condenser 616, an expansion valve 620 and an injectionmold 622, all fluidly connected by a plurality of cooling lines 612 a-dto form a closed loop cooling circuit 614. In the embodiment of FIG. 15,the injection mold 622 itself, and more specifically a mold supportplate of the injection mold 622, forms the evaporator.

Cooling fluid flowing through the injection mold 622 removes heat fromthe injection mold 622, thereby cooling molten plastic within theinjection mold 622. The increased cooling capacity of the evaporativecooling system 600 reduces cycle time of the injection mold 622 byremoving heat more quickly than traditional cooling systems that movecooling liquid only through cooling channels.

Turning now to FIG. 16A, another example of an evaporative coolingsystem 700, which is located in a mold support plate 478 of an injectionmold, is illustrated. The evaporative cooling system 700 includes achamber 710 within the mold support plate 478. An evaporative liquid712, such as water, is disposed within the chamber 710. A percolatortube 714 connects a reservoir portion 716 of the chamber 710 to acondensing portion 718 of the chamber 710. The percolator tube 714assists in moving water from the bottom of the chamber 710 to the top ofthe chamber 710. A cooled condenser 720 may be located near the top ofthe chamber 710. As heat from the mold side (which would be located tothe right in FIG. 16A) warms the mold support plate 478, liquid water inthe reservoir portion 716 evaporates and travels upwards through thechamber towards the condensing portion 718. This evaporation processremoves heat from the mold support plate 478 and thus, from the moldside adjacent the mold support plate 478. When the water vapor reachesthe condenser 720, heat again transfers from the water vapor to thecondenser 720, which causes the water vapor to condense back into liquidform. This liquid water then runs down the sides of the chamber 710towards the reservoir portion 716. Some of the liquid water willre-evaporate from the side walls of the chamber and some of the liquidwater will reach the reservoir portion 716 before re-evaporating. Toenhance evaporation from the side walls of the chamber 710, a coatingmay be applied to the side walls that enhances retention of liquid wateragainst the side walls by increasing surface tension between the liquidwater and the side walls. A controllable heat source 722 may optionallybe disposed within the mold support plate 478 (or be attached to themold support plate 478) to regulate the volume of water returned to thecondensing section 718 through the percolator tube 714.

FIG. 16B illustrates an alternate embodiment of an evaporative coolingsystem 800. Elements of the evaporative cooling system 800 like those ofthe evaporative cooling system 700 of FIG. 16A have reference numeralsthat are 100 greater than the elements in FIG. 16A. The main differencein the evaporative cooling system 800 of FIG. 16B is that an additionalcollection portion 830 is located within the chamber 810 verticallybetween the condensing portion 818 and the reservoir portion 816. Thecollection portion 830 may facilitate collection and re-evaporation ofliquid water for larger (or longer) mold support plates.

While not illustrated, the evaporative (and vapor compression) coolingsystems 500, 600, 700, and 800 of FIGS. 14, 15, 16A, and 16B may includea vacuum system to lower relative pressures of the cooling fluids.Lowering relative pressures of the cooling fluids lowers the evaporationtemperature for a given cooling fluid (all other factors being equal).Conversely, the evaporative (and vapor compression) cooling systems 500,600, 700, and 800 may include a pressurization system to increaserelative pressure of the cooling fluid. Raising relative pressure of thecooling fluid raises the evaporation temperature of a given coolingfluid (all other factors being equal). In this way, the evaporationtemperature may be tailored to the temperatures typically experienced bya particular mold.

Evaporative cooling systems may use many different types of coolingfluids, such as refrigerants (e.g., chlorofluorocarbons,chlorofluoroolefins, hydrochlorofluorocarbons, hydrochlorofluoroolefins,hydrofluorocarbons, hydrofluoroolefins, hydrochlorocarbons,hydrochloroolefins, hydrocarbons, hydroolefins, perfluorocarbons,perfluoroolefins, perchlorocarbons, perchloroolefins, andhalon/haloalkane, and blends thereof), water, glycol, propylene glycol,alcohol, or mercury. Other refrigerants having cooling capacities and/orphysical or chemical properties similar to the refrigerants listed abovemay also be used. Similarly, other cooling fluids that undergo a phasechange when exposed to temperatures between about 0° C. and about 200°C. at pressures between 0 psi (i.e., complete vacuum) and about 2000psi, may also be used. In some cases a surfactant may be added to thecooling fluid. Some evaporative cooling systems may utilize a vacuumsystem to create differential pressure, while other evaporative coolingsystems may utilize compressors to create differential pressure.

In yet other embodiments, the evaporative cooling system may employatmospheric liquid evaporation to remove heat. Because the disclosedmold assemblies are made of highly thermally conductive materials, insome cooling complexity level zero mold assemblies it is possible tosimply spray a cooling liquid on the outer surface of the mold supportplates or mold sides, which evaporates as the liquid absorbs heat,thereby cooling the mold support plate or the mold side. One type ofliquid that may be advantageously employed in these types of systems isdistilled water. Distilled water will completely evaporate withoutleaving any type of residue on the mold support plate or mold side. Insome embodiments, fins or radiator structures may be used to increasesurface area of the mold support plate or mold side to furtherfacilitate evaporation and heat removal.

One example embodiment of an evaporative cooling system 900 that employsatmospheric liquid evaporation is illustrated in FIG. 17. The mold 910may include a first mold side 925 and a second mold side 927. A firstmold support plate 978 and a second mold support plate 980 may belocated adjacent the first and second mold sides 925, 927, respectively.A spray bar 911 may be positioned near one of the mold support plates978, 980, and/or near one of the mold sides 925, 927. The spray bar 910is fluidly connected to a pump 912, which pumps liquid (for examplewater) to the spray bar 910 under pressure. The liquid is sprayed out ofa nozzle 914 so that the sprayed liquid coats an outer surface of one ofthe mold support plates 978, 980 and the mold sides 925, 927. As theliquid coats the outer surface, heat from the mold support plate 978,980, and/or the mold side 925, 927, causes the liquid to evaporate, thuscooling the mold support plate 978, 980 and/or the mold side 927, 927.Liquid that does not evaporate may drip down and collect in a liquidcollection area or sump 940. The sump 940 is an area or reservoir forcollecting liquid that does not evaporate. A return line 942 extendsfrom the sump 940 to the pump 912 to channel water from the sump 940back to the spray bar 911. The pump 912 may also be connected to asource of liquid 944 so that a supply of liquid is always available tothe spray bar 911, regardless of the level of liquid in the sump 940.

In the embodiment illustrated in FIG. 17, evaporated liquid simply ventsto the atmosphere and fresh liquid is supplied through the source ofliquid 944 to make up for the lost evaporated liquid. In otherembodiments, the entire mold 910 may be located in a closed environmentand the evaporated liquid may be condensed and returned to the sump 940.

The disclosed mold assemblies may include cooling systems having coolingchannels that are completely confined within a mold support plate. As aresult, the disclosed systems do not need any dynamic seals (e.g., sealsbetween moving parts) and the risk of cooling fluid escaping to theatmosphere, or being released into the environment is reduced.

As described above, the cooling systems disclosed herein, for a levelone cooling complexity mold, include cooling channels only in one ormore of the mold support plates. In other words, there are no coolingchannels in either the first mold side or the second mold side. As aresult, all seals in the cooling systems are static in nature and veryrobust. Stated another way, there are no seals between components thatmove relative to one another in the disclosed cooling systems, whichwould require softer, dynamic seals. Thus, the disclosed cooling systemsmay use dangerous, hazardous, or expensive cooling fluids (sometimesreferred to as “exotic cooling fluids”) as there is little chance ofseal breach, which would result in release of the cooling fluid. Somedangerous, hazardous, or expensive cooling fluids may have superior heatabsorption properties when compared to traditional cooling fluids.However, these dangerous, hazardous, or expensive cooling fluids havenot been previously used in cooling systems for injection molds for fearof seal breach (especially a breach in dynamic seals between movingparts), which would release these cooling fluids to the atmosphere.Particularly useful dangerous, hazardous, or expensive cooling fluidsthat may now be used in the disclosed cooling systems (due to the verylow risk of these cooling fluids escaping to the atmosphere) includeheating oil, hydraulic fluid, glycols, cesium, mercury, potassium (whichhas a thermal conductivity of approximately 42 W/mK at 25° C.),lead-bismuth eutectic, sodium potassium alloy, sodium potassium cesiumalloy, and lead-bismuth.

Desirable cooling fluids may have a thermal conductivity of 1 W/mK ormore. More desirable cooling fluids may have a thermal conductivity ofbetween about 1 W/mk to about 42 W/mk. Some desirable cooling liquidsmaintain a flowable viscosity (e.g., a cpi of 100,000 or less) attemperatures between about 5° C. and about 100° C. In addition tohazardous or dangerous cooling fluids, non-hazardous cooling fluids thatare relatively expensive may also be used in the disclosed coolingsystems. One such expensive, but useful, cooling fluid is distilledwater, which advantageously dose not corrode internal components of thedisclosed cooling systems. Distilled water, however, has not been usedin conventional high productivity injection molding systems because ofthe need to constantly replace distilled water lost through sealbreaches. These losses generally required a distillation plant on siteto produce make up distilled water, which is cost prohibitive in thehighly competitive consumer products injection molding industry.

By eliminating dynamic seals from the disclosed cooling complexity levelone molds, a wider range of cooling fluids may be used. As describedabove, some potentially harmful, hazardous, or expensive cooling fluidsmay be used. Additionally, nanofluids may be used as cooling fluids.Nanofluids include a carrier liquid, such as water, having tinynano-scale particles known as nanoparticles dispersed throughout thecarrier liquid. Nanoparticles of solid materials (e.g., copper oxide,alumina, titanium dioxide, carbon nanotubes, silica, or metals,including copper, or silver nanorods) may be dispersed into the carrierliquid, which enhances the heat transfer capabilities of the resultingcoolant compared to the carrier liquid alone. The enhancement can betheoretically as high as 350%. In some examples, nanofluids have beenexperimentally shown to have thermal conductivities of 50%-100% greaterthan the thermal conductivity of the carrier liquid alone. Nanofluidsalso exhibit a significant increase in heat flux when compared totraditional cooling fluids. In one example, a nanofluid may compriseethylene glycol and copper nanoparticles, which has a thermalconductivity of approximately 1.4 W/mK at 25° C.

For example, silver nanorods of 55±12 nm diameter and 12.8 μm averagelength at 0.5 vol. % can increase thermal conductivity of water by 68%,and 0.5 vol. % of silver nanorods increased thermal conductivity ofethylene glycol based coolant by 98%. Alumina nanoparticles at 0.1% canincrease the critical heat flux of water by as much as 70%.

Because the seals in level one cooling complexity molds are very robustin nature (because they are static seals), the seals are much moretolerant of the nanoparticles in nanofluids, which tend to degradedynamic (softer) seals more quickly. As a result, the disclosed coolingcomplexity level one molds may use nanofluids to increase heat transferrates, which results in more efficient cooling. Desirable nanofluids mayhave thermal conductivities of 1 W/mK or more. Examples of nanoparticlesthat may be added to a carrier fluid include copper oxide, alumina,titanium oxide, boron nitride nanotubes, carbon nanotubes, carbonuranium nano rods, and silver nano rods. Additionally, these nanofluidshave a greater heat capacity than traditional cooling fluids. As aresult, fluid circulation rates may be slowed to allow the nanofluid toremove more heat per unit volume than traditional cooling fluids. Thus,the overall cooling fluid volume needed for such a system may bereduced, causing a corresponding reduction in overall cost andcomplexity of the cooling system.

This increase in thermal conductivity and reduction in overall fluidvolume may allow some cooling complexity level one molds that usenanofluids to employ a radiant heat type heat exchanger to cool thenanofluid before circulation through the mold support plate, as thenanofluid would linger in the heat exchanger long enough to adequatelycool the nanofluid.

In some level zero cooling complexity molds, the mold may be cooledcompletely by convection/conduction of heat to the atmosphere. Radiatorfins may be formed on the mold support plates or the mold sides toenhance convection of heat to the atmosphere. Additionally, a gas movingdevice, such as a fan, may move atmospheric gases over the molds and/orover the radiator fins to further enhance heat dissipation thoughconduction.

Generally speaking, the low constant pressure injection molding machinesof the present disclosure include molds and/or mold assembliesmanufactured from materials having high thermal conductivity, asdiscussed above. This high thermal conductivity allows the disclosed lowconstant pressure injection molding machines, molds, and mold assembliesto cool molded parts using cooling complexity level three moldassemblies or lower for virtually any part geometry. Preferably acooling complexity level two mold assembly will be used to cool a moldedpart. More preferably a cooling complexity level one mold assembly willbe used to cool a molded part. For some part geometries, a coolingcomplexity level zero mold assembly may even be used. The coolingcomplexity level three or lower mold assemblies may be used even inultra high output consumer product injection molding machines (e.g.,class 101-102 injection molding machines) where more complex coolingsystems were needed for conventional injection molds made from highhardness, low thermal conductivity materials. As a result, the disclosedlow constant pressure injection molds and mold assemblies, and thus theinjection molding machines, are less costly to manufacture, whiledecreasing mold cycle times and increasing mold productivity due atleast in part to the availability of less complex cooling systems.

An additional benefit of molds made from high thermal conductivitymaterials is that a temperature profile for the mold is more uniformduring the injection molding process than in conventional molds. Inother words, there is less temperature variation from point to pointwithin the mold. As a result, parts manufactured in molds with highthermal conductivity have less internal stress (and a more uniformcrystalline structure) than parts manufactured in conventional molds.This lower internal stress and more uniform crystallinity result inlower rates of part warp. In conventional molds, the mold cavity isoften designed to offset part warp due to non-uniform temperaturegradients, which adds to the cost and complexity of conventional moldassemblies. Finalizing a particular offset usually requires an iterativeand time consuming trial process. In high thermal conductivity molds,the mold cavity need not be designed to offset warp because the moldedpart does not experience a significant amount of warp, as internalstresses are more uniform due to the more uniform cooling. Thus, theiterative offset process used in the design of conventional molds may beavoided, further reducing manufacturing costs and time.

It is noted that the terms “substantially,” “about,” and“approximately,” unless otherwise specified, may be utilized herein torepresent the inherent degree of uncertainty that may be attributed toany quantitative comparison, value, measurement, or otherrepresentation. These terms are also utilized herein to represent thedegree by which a quantitative representation may vary from a statedreference without resulting in a change in the basic function of thesubject matter at issue. Unless otherwise defined herein, the terms“substantially,” “about,” and “approximately” mean the quantitativecomparison, value, measurement, or other representation may fall within20% of the stated reference.

It should now be apparent that the various embodiments of the productsillustrated and described herein may be produced by a low constantpressure injection molding process. While particular reference has beenmade herein to products for containing consumer goods or consumer goodsproducts themselves, it should be apparent that the low constantpressure injection molding method discussed herein may be suitable foruse in conjunction with products for use in the consumer goods industry,the food service industry, the transportation industry, the medicalindustry, the toy industry, and the like. Moreover, one skilled in theart will recognize the teachings disclosed herein may be used in theconstruction of stack molds, multiple material molds includingrotational and core back molds, in combination with in-mold decoration,insert molding, in mold assembly, and the like.

All documents cited in the Detailed Description of the Invention are, inrelevant part, incorporated herein by reference; the citation of anydocument is not to be construed as an admission that it is prior artwith respect to the present invention. To the extent that any meaning ordefinition of a term in this written document conflicts with any meaningor definition of the term in a document incorporated by reference, themeaning or definition assigned to the term in this written documentshall govern.

While particular embodiments have been illustrated and described herein,it should be understood that various other changes and modifications maybe made without departing from the spirit and scope of the claimedsubject matter. Moreover, although various aspects of the claimedsubject matter have been described herein, such aspects need not beutilized in combination. It is therefore intended that the appendedclaims cover all such changes and modifications that are within thescope of the claimed subject matter.

What is claimed is:
 1. A mold assembly for an injection molding machine,the mold assembly comprising: a first mold side and a second mold side,the first mold side and the second mold side defining a mold cavitytherebetween; a first mold support plate being disposed one ofimmediately adjacent to or in direct contact with the first mold side; asecond mold support plate being disposed one of immediately adjacent toor in direct contact with the second mold side; and an evaporativecooling system for removing heat from one of the first and second moldsides during an injection molding process, the evaporative coolingsystem including one or more cooling fluid channels, wherein none of thecooling fluid channels of the evaporative cooling system extends intothe first mold side or the second mold side.
 2. The mold assembly ofclaim 1, wherein the evaporative cooling system includes a cooling fluidthat circulates in a closed-loop cooling circuit through one or morecooling fluid channels.
 3. The mold assembly of claim 2, wherein theclosed-loop cooling circuit is confined to one of the first mold supportplate and the second mold support plate.
 4. The mold assembly of claim3, wherein the one of the first mold support plate and the second moldsupport plate includes a projection and the corresponding first moldside or second mold side includes a complimentary recess that is sizedand shaped to receive the projection.
 5. The mold assembly of claim 1,wherein the evaporative cooling system includes a condenser coupled toone of the first mold support plate and the second mold support plate.6. The mold assembly of claim 1, wherein the evaporative cooling systemincludes a spray bar that sprays cooling fluid on a surface of one ofthe first mold support plate and the second mold support plate, thecooling fluid evaporating on the surface thereby extracting heat fromthe one of the first mold support plate and the second mold supportplate.
 7. The mold assembly of claim 1, wherein the first and secondmold sides are made from materials having a thermal conductivity ofgreater than 30 BTU/HR FT ° F.
 8. The mold assembly of claim 1, whereinone of the first mold support plate and the second mold support platehas an average thermal conductivity that is higher than the averagethermal conductivity of one of the first and second mold sides.
 9. Themold assembly of claim 1, wherein at least one of the first and secondmold sides is made of a material having an average surface hardness ofless than 30 Rc.
 10. The mold assembly of claim 1, wherein a mold cavitybetween the first and second mold sides defines a part having a wallthickness of less than about 2 mm.
 11. The mold assembly of claim 1,wherein at least one of the first and second mold sides is made fromaluminum.
 12. The mold assembly of claim 1, wherein at least one of thefirst and second mold sides is formed from a material having at leastone of, a milling machining index of greater than 100%, a drillingmachining index of greater than 100%, and a wire EDM machining index ofgreater than 100%.
 13. The mold assembly of claim 1 disposed in asubstantially constant low pressure injection molding system.
 14. Themold assembly of claim 1, further comprising a second cooling systemincluding a plurality of cooling channels extending into at least one ofthe first mold support plate, the second mold support plate, the firstmold side, and the second mold side, and the second cooling systemincluding circulating cooling liquid.
 15. The mold assembly of claim 1,further comprising at least one of, a mold cavity having an L/T ratio ofgreater than 100; at least four mold cavities; one or more heatedrunners; a balanced molten plastic feed system; and a guided ejectionsystem.
 16. A mold assembly for an injection molding machine, the moldassembly comprising: a first mold side and a second mold side, the firstmold side and the second mold side defining a mold cavity therebetween;a first mold support plate being disposed one of immediately adjacent toor in direct contact with the first mold side; a second mold supportplate being disposed one of immediately adjacent to or in direct contactwith the second mold side; a cooling system for removing heat from oneof the first and second mold sides during an injection molding process;and a cooling fluid disposed in the cooling system, the cooling fluidhaving a thermal conductivity of about 1 W/mK or greater.
 17. The moldassembly of claim 16, further comprising cooling channels that areconfined to one of the first and second mold support plates.
 18. A moldassembly for an injection molding machine, the mold assembly comprising:a first mold side and a second mold side, the first mold side and thesecond mold side defining a mold cavity therebetween; a first moldsupport plate one of immediately adjacent to or in direct contact withthe first mold side; a second mold support plate one of immediatelyadjacent to or in direct contact with the second mold side; anevaporative cooling system for removing heat from one of the first andsecond mold sides during an injection molding process, the evaporativecooling system having an evaporative cooling channel confined to thefirst or second mold support plate.
 19. The mold assembly of claim 18,wherein the evaporative cooling system includes a compressor, acondenser, and an expansion valve located outside of the first or secondmold support plate, the compressor, the condenser, and the expansionvalve being fluidly connected with one of the first and second moldsides.
 20. The mold assembly of claim 19, wherein the first mold supportplate is in complete contact with the first mold side or the second moldsupport plate is in complete contact with the second mold side.